|Publication number||US6183897 B1|
|Application number||US 09/153,959|
|Publication date||Feb 6, 2001|
|Filing date||Sep 16, 1998|
|Priority date||Sep 16, 1998|
|Also published as||DE69900574D1, DE69900574T2, EP0993059A2, EP0993059A3, EP0993059B1|
|Publication number||09153959, 153959, US 6183897 B1, US 6183897B1, US-B1-6183897, US6183897 B1, US6183897B1|
|Inventors||Joseph Jay Hartvigsen, Ashok Chandrashckhar Khandkar, Singaravelu Elangovan|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (10), Referenced by (61), Classifications (23), Legal Events (8)|
|External Links: USPTO, USPTO Assignment, Espacenet|
1. Field of the Invention
The present invention relates generally to the field of power generation and in particular to an improved interconnect for a solid oxide fuel cell.
2. Background of the Invention
Global demand for power generation in the next twenty years is expected to increase by about 2 million MW, of which 490,000 MW are projected to be powered by natural gas. Utility deregulation in the United States, concerns over health issues and capital costs associated with the transmission and distribution of electrical power make it likely that at least 30% of this natural gas fired capacity will be provided by modular power plants located in close proximity to the end users.
Solid oxide fuel cells are an attractive solution for meeting those needs for distributed power in a manner which is both energy efficient and environmentally sound. Solid oxide fuel cells offer modularity as well as higher fuel efficiency, lower emissions, and less noise and vibration than gas turbines or diesel generators. Data from test modules show that Nox production is greatly reduced and almost non-existent in fuel cells. At the same time, fuel cell test modules have been tested to operate at greater than 50% efficiency.
In order to be widely accepted by delivering energy efficiently and in an environmentally sound manner, solid oxide fuel cells must be able to cost-effectively produce electricity and heat. The capital and operating costs of solid oxide fuel cells must compare favorably with alternative sources for distributed power, such as internal combustion engines and gas turbines.
Interconnect functionality and cost are two of the biggest barriers to producing market competitive solid oxide fuel cell generators. The interconnect must provide reactant gas separation and containment, mechanical support to the cells and a low resistance path for current connecting the cells electrically in series and/or in parallel. Meeting these functional requirements remains a challenge. Monolithic interconnects made of lanthanum chromite and high chromium alloys have been used with some success. However, both types are quite expensive and compromise aspects of the interconnect function.
Lanthanum chromite and high chromium alloys are currently cost prohibitive for use in commercial products with a conventional monolithic interconnect design. Projected costs, assuming high production volumes using net shape ceramic processing or a metal forming process, are potentially low enough to enable marginally cost competitive solid oxide fuel cell power generation. However, the gap between required startup cost and initial market size is a decisive barrier to solid oxide fuel cell commercialization.
Gas separation requires a dense impermeable material which does not have significant ionic conductivity. Alloy interconnects that have been developed readily satisfy this requirement. Ceramic processing has developed the capability to produce interconnects of sufficiently high density, however, many compositions have unacceptably high ionic conductivity. The known compositions of such ceramics possessing low ionic conductivity also have less than acceptable electronic conductivity or are not well matched to the coefficient of thermal expansion (CTE) of the cell.
Matching cell and interconnect coefficients of thermal expansion allows sealing of cells to interconnects for gas containment. Alloy interconnects generally have a higher CTE than the CTE of the cell. While the CTE of ceramic interconnects are more nearly matched than alloy interconnects, they are still lower than that of the cell. As a result, regions of the cell may be adversely displaced wherein it becomes difficult to effectively confine reactant gases to their intended flow paths, which in turn adversely affects the stack efficiency. While changes between room and operating temperatures produce the largest thermal displacements, temperature changes in a stack as reactant and current flows are varied can also create undesirable detrimental displacements.
Dissimilar thermal expansion characteristics also cause the relative motion imparted by thermal expansion to disrupt the electrical current path between the electrodes and interconnects. The contact resistance generated in this way significantly reduces stack performance and efficiency. In the case of alloy interconnects, the motion can dislodge a protective oxide scale and expose underlying unprotected material. Oxidation of the unprotected material increases the overall scale thickness, and as scale conductivity is comparatively poor, scale growth contributes directly to performance degradation.
The issues presented by oxide scale conductivity and growth are some of the most challenging of all those confronting developers of metal interconnects. Scale resistance is a function of oxide conductivity, thickness and continuity. Porous or laminar scales have the effect of increasing the current path length while reducing the effective current carrying cross sectional area. The mechanism for scale conductivity and growth are related such that scale growth rate increases with scale conductivity. Higher growth rates generally produce less dense, less adherent scales. Any alloy (other than noble or semi-noble metals) will have to compromise scale conductivity in order to control degradation due to scale growth. Coating the interconnect with a conductive oxide layer provides more control of the scale composition and microstructure but does not change the basic nature of the problem.
Thus, it is an object of the present invention to provide an interconnect for a solid oxide fuel cell which permits substantial matching of cell and interconnect coefficients of thermal expansion.
It is a further object of the invention to provide an interconnect region manufactured using vias to fill the interconnect space between the cell anode and cathode to match the material coefficients of thermal expansion.
It is also an object of the invention to separate the interconnect functions of gas separation and containment, from the current carrying function of the interconnect, thereby enabling selection of materials best suited to each function and atmosphere.
The present invention comprises an interconnect for a solid oxide fuel cell comprising a gas separator plate and at least one fill material. The gas separator plate includes at least one via extending therethrough. The at least one fill material is positioned within the at least one via and is operatively associated with at least one of a cathode or an anode.
In a preferred embodiment, the interconnect includes at least an anode contact associated with the anode, and a cathode contact associated with the cathode. In either case, the contacts have coefficients of thermal expansion which are the same or substantially similar to the coefficient of thermal expansion of the associated fill material.
In another preferred embodiment, the at least one fill material comprises two fill materials, specifically, an anode fill material and a cathode fill material. The anode fill material is associated with the anode and the cathode fill material is associated with the cathode.
In yet another preferred embodiment, the at least one fill material includes at least one coefficient of thermal expansion. In such an embodiment, the interconnect may further comprise at least one anode contact that is associated with the anode, and at least one cathode contact that is associated with the cathode. The coefficient of thermal expansion of the at least one fill material is the same or substantially similar to that of at least one of the anode contact or the cathode contact. In this preferred embodiment, the fill material is directly associated with the respective anode and/or cathode contact. Accordingly, the coefficient of thermal expansion of the fill material will substantially match that of the associated anode and/or cathode contact.
In a preferred embodiment, the anode fill material is one of silver-palladium and a mixture of a high chromium alloy (such as is commercially manufactured by PLANSEE, A.G. of Austria, and wherein such a mixture is hereinafter identified as “PLANSEE”) via a powder metal process and doped lanthanum chromite (hereinafter identified as “LSMC”) and the gas separator plate may comprise a yttria stabilized zirconia (3YSZ). The cathode fill material may comprise one of lanthanum strontium manganite and a mixture of LSMC and lanthanum cobaltite (hereinafter identified as “LSCo”).
In such a preferred embodiment, the anode contact may comprise one of nickel, PLANSEE and LSMC, and the cathode contact may comprise one of silver-palladium, lanthanum strontium manganite and LSCo.
The invention further includes a method for manufacturing an interconnect for a solid oxide fuel cell. The method comprises the steps of: (a) providing a gas separator plate; (b) forming at least one via through the gas separator plate; (c) introducing at least one fill material into the at least one via; and (d) operatively associating at least one of a cathode or anode with the at least one fill material.
In a preferred embodiment, the method further comprises the step of: (a) associating at least one of an anode contact and/or a cathode contact with one end of the at least one via. The coefficient of thermal expansion thereof is the same or substantially similar to the thermal expansion of the at least one fill material. Of course, it is likewise contemplated that both the anode contact and cathode contact can be operatively associated with corresponding portions of the fill material, and that the respective coefficients of thermal expansion are the same or substantially similar
In another preferred embodiment, the step of introducing the at least one fill material comprises the steps of: (a) placing a metal ink into the at least one via; and (b) sintering the metal ink to density.
In the drawings:
FIG. 1 is a side elevational view of a section of a solid oxide fuel cell stack having an interconnect according to the invention.
FIG. 2 is a side elevational view of a interconnect of the stack of FIG. 1;
FIG. 3 is an enlarged view of the region A shown in FIG. 2;
FIG. 4 is a top plan view of the interconnect used in the cell stack of FIG. 1; and
FIG. 5. is a schematic of the method of manufacturing the interconnect.
While this invention is susceptible of embodiment in many different forms, there is shown in the drawings and will herein be described in detail, one specific embodiment, with the understanding that the present disclosure is to be considered as an exemplification of the principles of the invention and is not intended to limit the invention to the embodiment illustrated.
A portion of solid oxide fuel cell stack 10 is shown in FIG. 1 as comprising a monolithic structure that includes a plurality of trilayer cells, such as trilayer cell 15 and a via-filled interconnect such as via-filled interconnect 17 positioned between any two trilayer cells. While the embodiment of FIG. 1 is shown as comprising a stack having three trilayer cells and two interconnects, it is likewise contemplated that, depending on the requirements for the particular application, a particular cell may comprise any number of trilayer cells (and corresponding interconnects) having any one of a number of varying shapes and sizes.
As shown in FIG. 1, each trilayer cell, such as trilayer cell 15, includes anode 40, electrolyte 41 and cathode 42. As will be understood, the anode, the electrolyte and the cathode may comprise a variety of combinations of materials which are well known in the art.
As shown in FIGS. 1 and 2, each via-filled interconnect, such as via-filled interconnect 17 (FIG. 2) comprises gas separator plate 22, fill material 24, cathode contact 26, anode contact 28 and seals 30, 32 (FIG. 1). Gas separator plate 22, as shown in FIGS. 1-3, comprises a ceramic material which includes a plurality of vias, such as via 60. Gas separator plate may comprise a single or multi-layer ceramic substrate. Moreover, many different ceramic compositions may be utilized for the gas separator plate, so long as they are gas impermeable, have minimal ionic conductivity and can withstand the operating temperatures of the fuel cell, as will be understood by one of skill in the art. For example, and while not limited thereto, the interconnect may comprise a yttria stabilized zirconia, such as 3 mole percent Y2O3 (3YSO).
Vias, such as via 60, are shown in FIGS. 2-4 as comprising openings that extend through the one or more layers that comprise the gas separator plate 22. Various dimensions and shapes of the via are contemplated, as well as both uniform and non-uniform crosssectional configurations.
As shown in FIG. 3, fill material 24 includes cathode via fill 36 and anode via fill 38, both of which are positioned within each of vias 60. The cathode via fill and the anode via fill 38 connect at interface 65, to, in turn, provide an electrical connection through the interconnect.
While other configurations are contemplated, the anode fill material has a coefficient of thermal expansion closely matched with the anode contact. Similarly, the cathode fill material has a coefficient of thermal expansion closely matched with the cathode contact. Thus, as the cell operates and thermally expands/contracts, the cell will be free from undesirable distortion. The particular materials utilized for the cathode and the anode fill material will vary and will generally depend on the cathode/anode material that is utilized. For example, cathode via fill 36 may comprise lanthanum strontium manganite, a mixture of PLANSEE and LSMC or a mixture of lSMC and LSCo. Anode via fill 38 may comprise nickel, silver-palladium alloy or a mixture of PLANSEE and LSMC or a mixture of PLANSEE and LSMC. In addition, in certain situations, it is contemplated that both the cathode fill material and the anode fill material may comprise an identical composition, in which case the vias are filled with a single material composition, such as doped chromite, silver-palladium or PLANSEE.
As shown in FIG. 1-3, cathode via fill 36 is electrically connected with cathode contact 26. In particular, as shown in FIG. 1, the cathode contact, through a cathode bond layer 47, is, in turn, bonded to cathode 42″ of trilayer cell 15″. Similarly, anode via fill 38 is electrically connected with the anode contact 28. The anode contact, through anode bond layer 45, is, in turn bonded to anode 40′ of another one of the trilayer cells, such as trilayer cell 15′. While various materials for each of the cathode contact and the anode contact are contemplated, the anode contact may comprise nickel, PLANSEE, silver-palladium or LSMC and the cathode contact may comprise silver palladium, lanthanum strontium manganite, LSM or LSCo.
As also shown in FIG. 1, the relative positioning of the anode contacts between the anode and the gas separator plate defines passageway 52 which facilitates the passage of fuel therethrough. Similarly, the relative positioning of the cathode contacts between the cathode and the gas separator plate defines passageway 50 which facilitates the passage of air therethrough. Seal 30 and seal 32 prevent the air and the fuel, respectively, from undesirably exiting from the respective air and fuel passages. While other materials are contemplated, the seals may comprise a material substantially similar to that of gas separator plate 22.
The manufacture of the cell comprises the assembly of the desired quantity of trilayer cells with the required interconnects. As shown schematically in FIG. 5, the interconnects are manufactured by first selecting the contemplated material for gas separator plate 22. Once separator plate 22 is formed, vias 60 are formed therethrough. One particular pattern for the vias 60 is shown in FIG. 4. Of course, various other patterns for the positioning and orientation of vias that extend through separator plate 22 are likewise contemplated.
Once the vias are formed through separator plate 22, cathode via fill 36 and anode via fill material 38 are each selected. As explained above, the materials are selected based upon their relative coefficients of thermal expansion and the coefficient of thermal expansion of the respective anode or cathode material (or anode contact and cathode contact material). Once selected, the anode via fill and the cathode via fill are introduced into each via. While other processes are contemplated, one maimer in which to introduce the fill into each via comprises the filling of the via with a desired cathode metal ink 80 and a desired anode metal ink 82 and subsequently sintering the material to density. Where the anode via fill and the cathode via fill comprise identical materials, a single material is introduced into the entire via. Once the vias have been filled with the appropriate fill material, anode contact 28 and cathode contact 26, respectively, are connected to complete the assembly of the interconnect. Lastly, the interconnects, the seals and the trilayer cells are assembled in a monolithic construction so as to render completed stacked cell 10, as shown in FIG. 1.
In operation, as the cell thermally expands or contracts through temperature changes due to the operation of the cell and due to external influences on the cell, the via fill material likewise expands or contracts at a rate which is substantially identical to the respective anode or cathode (or anode contact or cathode contact). Thus, throughout the expansion or contraction the fill material and the anode/cathode/contacts can expand or contract at a similar rate. This serves to maintain the integrity of the cell, and prevents distortion which lessens the efficiency of the cell. In addition, the use of both the desired via fill material and the desired gas separator plate material allows the cell to advantageously utilize the benefits of each of the materials.
The foregoing description and drawings merely explain and illustrate the invention and the invention is not limited thereto except insofar as the appended claims are so limited, as those skilled in the art who have the disclosure before them will be able to make modifications and variations therein without departing from the scope of the invention.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US3717506 *||Jan 28, 1971||Feb 20, 1973||Us Army||High voltage deposited fuel cell|
|US4510212 *||Oct 12, 1983||Apr 9, 1985||The United States Of America As Represented By The United States Department Of Energy||Solid oxide fuel cell having compound cross flow gas patterns|
|US4666798 *||May 20, 1985||May 19, 1987||The United States Of America As Represented By The United States Department Of Energy||Serially connected solid oxide fuel cells having monolithic cores|
|US5063122 *||Apr 24, 1990||Nov 5, 1991||Asea Brown Boveri Aktiengesellschaft||Fuel cell assembly comprising permanently combined fuel cells|
|US5273837 *||Dec 23, 1992||Dec 28, 1993||Corning Incorporated||Solid electrolyte fuel cells|
|US5501914 *||Aug 26, 1994||Mar 26, 1996||Mitsubishi Jukogyo Kabushiki Kaisha||Solid oxide electrolyte fuel cell|
|US5614127 *||Feb 28, 1995||Mar 25, 1997||Gas Research Institute||High-performance ceramic interconnect for SOFC applications|
|US5789093 *||Dec 10, 1996||Aug 4, 1998||Texas Instruments Incorporated||Low profile fuel cell|
|US5827620||Mar 17, 1994||Oct 27, 1998||Keele University||Solid oxide fuel cell structures|
|WO1994022178A2||Mar 17, 1994||Sep 29, 1994||Keele University||Solid oxide fuel cell structures|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US6623881||May 15, 2001||Sep 23, 2003||Corning Incorporated||High performance solid electrolyte fuel cells|
|US6749775||Jan 29, 2002||Jun 15, 2004||Cts Corporation||Conductive via composition|
|US6824907||Feb 14, 2002||Nov 30, 2004||Alberta Reasearch Council, Inc.||Tubular solid oxide fuel cell stack|
|US6846588||Jan 16, 2002||Jan 25, 2005||Alberta Research Council Inc.||Hollow inorganic membranes produced by metal or composite electrodeposition|
|US6852436||Feb 15, 2002||Feb 8, 2005||Corning Incorporated||High performance solid electrolyte fuel cells|
|US6893762||Jul 25, 2002||May 17, 2005||Alberta Research Council, Inc.||Metal-supported tubular micro-fuel cell|
|US6958196||Feb 21, 2003||Oct 25, 2005||Trustees Of The University Of Pennsylvania||Porous electrode, solid oxide fuel cell, and method of producing the same|
|US7074255||Mar 16, 2004||Jul 11, 2006||Meacham G B Kirby||Noble metal gas barriers|
|US7175931 *||May 19, 2001||Feb 13, 2007||Forschungszentrum Julich Gmbh||Interconnector plate with openings and contact elements sealed in the openings|
|US7378173 *||Apr 24, 2003||May 27, 2008||Corning Incorporated||Fuel cells with enhanced via fill compositions and/or enhanced via fill geometries|
|US7452622||Jul 24, 2003||Nov 18, 2008||Alberta Research Council Inc.||Metal-supported tubular fuel cell|
|US7575821 *||Jun 11, 2002||Aug 18, 2009||General Electric Company||Interconnect supported fuel cell assembly and preform|
|US7651810||Jan 26, 2010||General Electric Company||Interconnect supported fuel cell assembly, preform and method of fabrication|
|US7736772||Feb 14, 2003||Jun 15, 2010||Alberta Research Council, Inc.||Tubular solid oxide fuel cell stack|
|US7846264 *||Nov 3, 2006||Dec 7, 2010||Applied Materials, Inc.||Cleaning method used in removing contaminants from a solid yttrium oxide-containing substrate|
|US7858261||May 2, 2006||Dec 28, 2010||Lilliputian Systems, Inc.||Systems and methods for stacking fuel cells|
|US7897292||Apr 10, 2006||Mar 1, 2011||Lilliputian Systems, Inc.||Fuel cell apparatus and methods|
|US8273485||Sep 25, 2012||Lilliputian Systems, Inc.||Fuel cell apparatus and methods|
|US8313875||Oct 2, 2006||Nov 20, 2012||Versa Power Systems, Ltd.||High performance cathode with controlled operating temperature range|
|US8383280||Feb 26, 2013||Amir Niroumand||Fuel cell separator plate with integrated heat exchanger|
|US8685589||Mar 12, 2008||Apr 1, 2014||Corning Incorporated||Fuel cells with enhanced via fill compositions and/or enhanced via fill geometries|
|US8709674||Dec 15, 2005||Apr 29, 2014||Alberta Research Council Inc.||Fuel cell support structure|
|US8962219||Nov 16, 2012||Feb 24, 2015||Bloom Energy Corporation||Fuel cell interconnects and methods of fabrication|
|US8986905||Nov 11, 2008||Mar 24, 2015||Bloom Energy Corporation||Fuel cell interconnect|
|US9190669||Jul 17, 2007||Nov 17, 2015||Versa Power Systems, Ltd.||Cell materials variation in SOFC stacks to address thermal gradients in all planes|
|US9263749 *||Sep 18, 2013||Feb 16, 2016||Murata Manufacturing Co., Ltd.||Fuel cell|
|US9287575 *||Sep 23, 2013||Mar 15, 2016||Murata Manufacturing Co., Ltd.||Fuel cell|
|US20020102450 *||Feb 15, 2002||Aug 1, 2002||Badding Michael E.||High performance solid electrolyte fuel cells|
|US20030113609 *||May 19, 2001||Jun 19, 2003||Peter Batfalsky||Device for electrically contacting electrodes in high-temperature fuel cells|
|US20030134171 *||Jul 25, 2002||Jul 17, 2003||Partho Sarkar||Metal-supported tubular micro-fuel cell|
|US20030141488 *||Jan 29, 2002||Jul 31, 2003||Bloom Terry R.||Conductive via composition|
|US20030228513 *||Jun 11, 2002||Dec 11, 2003||General Electric Company||Interconnect supported fuel cell assembly, preform and method of fabrication|
|US20040028975 *||Apr 24, 2003||Feb 12, 2004||Badding Michael E.||Fuel cells with enhanced via fill compositions and/or enhanced via fill geometries|
|US20040166380 *||Feb 21, 2003||Aug 26, 2004||Gorte Raymond J.||Porous electrode, solid oxide fuel cell, and method of producing the same|
|US20040185327 *||Dec 16, 2003||Sep 23, 2004||Gorte Raymond J.||High performance ceramic anodes and method of producing the same|
|US20050092175 *||Oct 29, 2003||May 5, 2005||Meacham G.B. K.||Noble metal gas barriers|
|US20050214613 *||Feb 14, 2003||Sep 29, 2005||Partho Sarkar||Tubular solid oxide fuel cell stack|
|US20050227134 *||Apr 13, 2004||Oct 13, 2005||Ion American Corporation||Offset interconnect for a solid oxide fuel cell and method of making same|
|US20060040168 *||Aug 19, 2005||Feb 23, 2006||Ion America Corporation||Nanostructured fuel cell electrode|
|US20060051643 *||Jul 24, 2003||Mar 9, 2006||Alberta Research Council Inc.||Metal-supported tubular fuel cell|
|US20060051661 *||Nov 14, 2003||Mar 9, 2006||Meacham G B Kirby||Diffusion stabilized gas barriers|
|US20060096453 *||Mar 16, 2004||May 11, 2006||Meacham G B K||Noble metal gas barriers|
|US20060246337 *||Dec 15, 2005||Nov 2, 2006||Partho Sarkar||Fuel cell support structure|
|US20060263655 *||May 18, 2006||Nov 23, 2006||Lilliputian Systems Inc.||Fuel cell apparatus and methods|
|US20060263665 *||Apr 10, 2006||Nov 23, 2006||Lilliputian Systems Inc.||Fuel cell apparatus and methods|
|US20070037031 *||Jul 12, 2006||Feb 15, 2007||Ion America Corporation||Cermet and ceramic interconnects for a solid oxide fuel cell|
|US20070151581 *||Nov 3, 2006||Jul 5, 2007||Applied Materials, Inc.||Cleaning method used in removing contaminants from a solid yttrium oxide-containing substrate|
|US20070259242 *||May 2, 2006||Nov 8, 2007||Lilliputian Systems Inc.||Systems and methods for stacking fuel cells|
|US20080081229 *||Jul 17, 2007||Apr 3, 2008||Versa Power Systems, Ltd.||Cell materials variation in SOFC stacks to address thermal gradients in all planes|
|US20080081243 *||Oct 2, 2006||Apr 3, 2008||Versa Power Systems, Ltd.||High performance cathode with controlled operating temperature range|
|US20080160376 *||Mar 12, 2008||Jul 3, 2008||Badding Michael E||Fuel cells with enhanced via fill compositions and/or enhanced via fill geometries|
|US20080193816 *||Aug 7, 2007||Aug 14, 2008||Schaevitz Samuel B||Fuel cell with substrate-patterned lower electrode|
|US20090071931 *||Jun 3, 2007||Mar 19, 2009||General Electric Company||Interconnect supported fuel cell assembly, preform and method of fabrication|
|US20100040924 *||Aug 12, 2009||Feb 18, 2010||Amir Niroumand||Fuel cell separator plate with integrated heat exchanger|
|US20100119909 *||Nov 11, 2008||May 13, 2010||Bloom Energy Corporation||Fuel cell interconnect|
|US20140017596 *||Sep 18, 2013||Jan 16, 2014||Murata Manufacturing Co., Ltd.||Fuel cell|
|US20140023955 *||Sep 23, 2013||Jan 23, 2014||Murata Manufacturing Co., Ltd.||Fuel cell|
|US20140178797 *||Feb 21, 2013||Jun 26, 2014||Samsung Electro-Mechanics Co., Ltd.||Solid oxide fuel cell|
|EP2690694A1 *||Mar 23, 2012||Jan 29, 2014||Murata Manufacturing Co., Ltd.||Fuel cell|
|EP2690694A4 *||Mar 23, 2012||Sep 3, 2014||Murata Manufacturing Co||Fuel cell|
|WO2001089017A1 *||May 11, 2001||Nov 22, 2001||Corning Incorporated||High performance solid electrolyte fuel cells|
|U.S. Classification||429/465, 264/214, 429/508, 429/535, 429/496, 429/495|
|International Classification||H01M8/24, H01M8/02, H01M8/12|
|Cooperative Classification||Y02P70/56, Y02E60/525, Y02E60/50, H01M8/0217, H01M8/0208, H01M8/0247, H01M2300/0074, H01M8/0256, H01M2008/1293, H01M8/2425|
|European Classification||H01M8/24B2H, H01M8/02C2A2, H01M8/02C2D2, H01M8/02C6V|
|Sep 16, 1998||AS||Assignment|
Owner name: SOFCO, UTAH
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:HARTVIGSEN, JOSEPH JAY;KHANDKAR, ASHOK CHANDRASHEKHAR;ELANGOVAN, SINGARAVELU;REEL/FRAME:009469/0865
Effective date: 19980916
|Aug 6, 2004||FPAY||Fee payment|
Year of fee payment: 4
|Jul 11, 2006||AS||Assignment|
Owner name: SOFCO-EFS HOLDINGS LLC, OHIO
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SOFCO, L.P.;REEL/FRAME:017906/0726
Effective date: 20060629
|Oct 12, 2007||AS||Assignment|
Owner name: ROLLS-ROYCE FUEL CELL SYSTEMS (USA) INC., OHIO
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SOFCO-EFS HOLDINGS LLC;MCDERMOTT TECHNOLOGY, INC;BWX TECHNOLOGIES, INC.;REEL/FRAME:019943/0796
Effective date: 20070330
|Jul 17, 2008||FPAY||Fee payment|
Year of fee payment: 8
|Jul 20, 2012||AS||Assignment|
Owner name: ROLLS-ROYCE FUEL CELL SYSTEMS (US) INC., OHIO
Free format text: CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE NAME OF ROLLS-ROYCE FUEL CELL SYSTEMS (USA) INC. PREVIOUSLY RECORDED ON REEL 019943 FRAME 0796. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNEE NAME SHOULD BE ROLLS-ROYCE FUEL CELL SYSTEMS (US) INC.;ASSIGNORS:SOFCO-EFS HOLDINGS LLC;MCDERMOTT TECHNOLOGY, INC.;BWX TERCHNOLOGIES, INC.;REEL/FRAME:028604/0475
Effective date: 20070327
|Aug 2, 2012||FPAY||Fee payment|
Year of fee payment: 12
|Oct 24, 2014||AS||Assignment|
Owner name: LG FUEL CELL SYSTEMS INC., OHIO
Free format text: CHANGE OF NAME;ASSIGNOR:ROLLS-ROYCE FUEL CELL SYSTEMS (US) INC.;REEL/FRAME:034046/0471
Effective date: 20120627